U.S. patent number 3,699,191 [Application Number 05/116,236] was granted by the patent office on 1972-10-17 for process for black copolymerization of polar monomers with an organolithium compound and heterocyclic sulfur compound.
This patent grant is currently assigned to The B. F. Goodrich Company. Invention is credited to Theodore F. Niemann.
United States Patent |
3,699,191 |
Niemann |
October 17, 1972 |
PROCESS FOR BLACK COPOLYMERIZATION OF POLAR MONOMERS WITH AN
ORGANOLITHIUM COMPOUND AND HETEROCYCLIC SULFUR COMPOUND
Abstract
Polar monomers can be polymerized to obtain block copolymers by
the sequential addition of the polar monomers. The polymerization
is initiated with an organolithium compound in combination with a
heterocyclic compound containing a sulfur heteroatom.
Acrylonitrile, methacrylonitrile and alkyl acrylates and
methacrylates are copolymerized to two- and three-block copolymers
with an initiator system consisting of an alkyl lithium compound
and a five- or six-membered heterocyclic compound or fused
heterocyclic ring system derived therefrom, where the heteroatom is
sulfur which may be unsubstituted or contain one or two oxygen
atoms bonded thereto but external to the ring.
Inventors: |
Niemann; Theodore F.
(Brecksville, OH) |
Assignee: |
The B. F. Goodrich Company (New
York, NY)
|
Family
ID: |
25339862 |
Appl.
No.: |
05/116,236 |
Filed: |
February 17, 1971 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
|
862961 |
Oct 1, 1969 |
3609100 |
|
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|
Current U.S.
Class: |
525/272; 525/308;
525/309 |
Current CPC
Class: |
C08F
297/026 (20130101) |
Current International
Class: |
C08F
297/00 (20060101); C08F 297/02 (20060101); C08f
015/38 (); C08f 015/16 (); C08f 015/22 () |
Field of
Search: |
;260/881 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Tillman; Murray
Assistant Examiner: Seibert; John
Parent Case Text
This is a division of application Ser. No. 862,961, filed Oct. 1,
1969, now U.S. Pat. 3,609,100.
Claims
I claim:
1. A process for the block copolymerization of polar monomers
comprising sequentially polymerizing two or more polar monomers
selected from the group consisting of acrylonitrile,
methacrylonitrile and alkyl esters of acrylic acid or methacrylic
acid wherein the alkyl group contains from one to eight carbon
atoms at a temperature between about -80.degree. C. and 50.degree.
C. with (1) an organolithium compound of the formula R--Li).sub.x
wherein R is an aliphatic, aromatic or cycloaliphatic hydrocarbon
radical containing from one to 12 carbon atoms and x is 1 or 2; and
(2) a heterocyclic compound selected from the group consisting of
five- and six-membered heterocycles and fused ring systems of five-
and six-membered heterocycles wherein the heteroatom is a sulfur
atom, said heterocyclic compound containing only carbon, hydrogen
and sulfur, with the sulfur atom being unsubstituted or substituted
with one or two oxygen atoms; the molar ratio of (2) to (1) being
from about 3:1 to about 0.5:1.
2. The block copolymerization process of claim 1 wherein the
concentration of (1) is between about 20 to 500 millimols per mol
of the initial polar monomer charge.
3. The block copolymerization process of claim 2 wherein the
concentration of (1) is between about 80 and 120 millimols per mol
of the initial polar monomer charge and (1) and (2) are present in
essentially a 1:1 molar ratio and which is conducted in an
aromatic, paraffinic or cycloparaffinic hydrocarbon solvent medium
at a temperature between about -60.degree.C. and 10.degree.C.
4. The block copolymerization process of claim 2 wherein (1) is an
alkyl lithium compound wherein the alkyl group contains from one to
six carbon atoms and (2) is selected from the group consisting of
dibenzothiophene, dibenzothiophene 5-oxide and dibenzothiophene
5,5-dioxide.
5. The block copolymerization process of claim 4 conducted in an
aromatic, paraffinic or cycloparaffinic hydrocarbon solvent medium
with a concentration of (1) between about 80 and 120 millimols per
mol initial monomer charge.
6. The block copolymerization process of claim 5 wherein the polar
monomers are methyl methacrylate and methacrylonitrile, (1) is
n-butyl lithium and (1) and (2) are present in essentially a 1:1
molar ratio.
7. The block copolymerization process of claim 6 which is conducted
in toluene at a temperature between about -60.degree.C. and
10.degree.C.
Description
BACKGROUND OF THE INVENTION
Anionic polymerization of nonpolar monomers to obtain block
polymers is known. Such polymerizations are typically conducted by
the sequential addition of the nonpolar monomers into the anionic
polymerization media or the anionic polymerization of mixtures of
the monomers. Organolithium compounds generally function as
initiators for these polymerizations.
The same anionic polymerization techniques are not generally
applicable, however, for the formation of block polymers when polar
monomers are to be employed. In the presence of polar monomers
termination of the growing polymer chain results and low molecular
weight polymers having little or no utility are obtained.
Variations in catalyst concentration, catalyst type, polymerization
media and polymerization temperature have been studied in an effort
to obtain useful block polymers with polar monomers, however, no
completely acceptable method has been reported. n-Butyl lithium has
been employed under a variety of polymerization conditions for the
homopolymerization of polar monomers, including methacrylonitrile
and methyl methacrylate, but two- and three- block copolymers of
methacrylonitrile and methyl methacrylate were not obtained
employing these same polymerization techniques.
SUMMARY OF THE INVENTION
I have now discovered an effective initiator system for the block
copolymerization of polar monomers. The present process and
initiator system permit the copolymerization of polar monomers such
as acrylonitrile, methacrylonitrile or alkyl acrylates and
methacrylates to obtain two- and three-block copolymers. The
process consists of the sequential addition of the polar monomers
to the polymerizing media containing an initiator system comprising
an organolithium compound and a heterocyclic compound containing a
sulfur heteroatom. Sulfur-containing heterocyclics will be five- or
six-membered ring compounds, saturated or containing unsaturation,
wherein the sulfur heteroatom may be unsubstituted or contain one
or two oxygen atoms bonded thereto but which are not a part of the
ring. The process will ordinarily be conducted in an inert
hydrocarbon solvent. The molar ratio of the heterocyclic compound
to the organolithium compound will generally range between about
3:1 to about 0.5:1. About 20 to about 500 millimols organolithium
compound per mol of the initial monomer charged will be employed to
initiate the polymerization.
DETAILED DESCRIPTION
The present invention relates to the block copolymerization of
polar monomers. The polymerization is initiated with an
organolithium compound in combination with a heterocyclic compound
wherein the heteroatom is sulfur. The organolithium compounds
employed are of the general formula R--Li).sub.x wherein R is an
aliphatic, aromatic or cycloaliphatic hydro-carbon radical
containing from one to 12 carbon atoms and x is 1 or 2. Typical
organolithium compounds include: methyl lithium, isobutyl lithium,
n-butyl lithium, sec-butyl lithium, t-octyl lithium, n-decyl
lithium, phenyl lithium, naphthyl lithium, 4-butyl lithium p-tolyl
lithium, cyclohexyl lithium, 4-butylcyclohexyl lithium and the
like, or mixtures thereof. Excellent results have been obtained
with alkyl lithium compounds wherein the alkyl group contains one
to six carbon atoms. In addition to organolithium compounds,
organosodium or organopotassium compounds may be employed for the
polymerization.
In preparing two- or three-block copolymers, organolithium
compounds containing one carbon-metal bond are most often employed
and the monomers to be polymerized are added sequentially. This
produces polymer anions propagating or growing at one end only.
Organolithium compounds containing two or even more carbon-metal
bonds, such as 1,5-dilithiopentane, may be advantageously employed,
however. These dimetallic initiators yield polymer anions
propagating at two ends so that for each increment of monomer added
after the first, two additional block segments will be formed. The
di-metallic initiators are an especially convenient means for
preparing three-block copolymer systems.
In combination with the organolithium compound to form the
initiator system of the present invention is a five- or
six-membered heterocyclic compound or a fused ring system derived
from a five- or six-membered heterocyclic compound wherein the
heteroatom is a sulfur atom. The heterocyclic compound may be
completely saturated or contain unsaturation. Only one sulfur
heteroatom will be present in the monocyclic or fused ring systems.
The sulfur heteroatom may be unsubstituted, such as in
dibenzothiophene, or it may be substituted with one or two oxygen
atoms, such as in dibenzothiophene 5-oxide or dibenzothiophene
5,5-dioxide. The oxygen atoms bonded to the sulfur heteroatom will
not be a part of the ring structure.
Useful heterocyclic compounds of the above type include thiophene,
thiophene 1-oxide, thiophene 1,1-dioxide, tetrahydrothiophene
1-oxide, tetrahydrothiophene 1,1-dioxide, .DELTA..sup.2
-dihydrothiophene 1-oxide, .DELTA..sup.2 -dihydrothiophene
1,1-dioxide, .DELTA..sup.3 -dihydrothiophene 1-oxide, .DELTA..sup.3
-dihydrothiophene 1,1-dioxide, .alpha.-thiapyran 1-oxide,
.alpha.-thiapyran 1,1-dioxide, .gamma.-thiapyran 1-oxide,
.gamma.-thiapyran 1,1-dioxide, .DELTA..sup.2 -dihydrothiapyran
1-oxide, .DELTA..sup.2 -dihydrothiapyran 1,1-dioxide, .DELTA..sup.3
-dihydrothiapyran 1-oxide, .DELTA..sup.3 -dihydrothiapyran
1,1-dioxide, thianaphthene, thianaphthene 1-oxide, thianaphthene
1,1-dioxide, .DELTA..sup.2 -dihydrothianaphthene 1-oxide,
.DELTA..sup.2 -dihydrothianaphthene 1,1-dioxide,
tetrahydrothia-naphthene 1-oxide, tetrahydrothianaphthene
1,1-dioxide, isothianaphthene, isothianaphthene 2-oxide,
isothianaphthene 2,2-dioxide, 1,3-dihydroisothianaphthene,
1,3-dihydroisothianaphthene 2,2-dioxide,
tetrahydroisothianaphthene, tetrahydroiso-thianaphthene 2-oxide,
dibenzothiophene, dibenzothiophene 5-oxide, dibenzothiophene
5,5-dioxide or the like. Especially useful heterocyclic compounds
for the present process are five-membered ring compounds or fused
ring systems derived therefrom such as thiophene and
dibenzothiophene and their derivatives. Excellent results have been
obtained when dibenzothiophene, dibenzothiophene 5-oxide and
dibenzothiophene 5,5-dioxide are employed.
The amount of the organolithium component employed will range
between about 20 and 500 millimols per mol of the initial monomer
charged and more preferably between 80 and 120 millimols per mol.
The amount of initiator governs the molecular weight of the initial
polymer block and may be varied accordingly. The organolithium
compound and the heterocyclic compound will generally be present in
essentially a 1:1 molar ratio. Molar ratios from about 3:1 to about
0.5:1 of the heterocyclic compound to the organolithium compound
can be employed, however. It is often advantageous to employ a
slight molar excess of the organolithium compound to serve as a
scavenger in the polymerization system for the removal of any
impurities which may be present.
In conducting the polymerizations the initiator system is utilized
in a hydrocarbon solvent medium such as aromatic, paraffinic or
cycloparaffinic hydrocarbons. Typically the same solvent employed
for the polymerization medium will be used to make up the initiator
solution. More often, however, the initiator components are
individually charged to the polymerizer before the initial monomer
charge. Useful hydrocarbons include propane, isobutane, n-pentane,
isopentane, cyclopentane, hexane, cyclohexane, benzene, toluene,
xylene or the like, and mixtures thereof.
The temperature of polymerization can range between about
-80.degree. C. to about 50.degree. C. depending on the monomers
employed. Excellent results have been obtained with the initiator
system of this invention at temperatures between about -60.degree.
C. and 10.degree. C. As various monomers are polymerized to form
the block segments, the polymerization temperature may be varied as
required. It is essential for the present process that a living
polymer be maintained throughout the polymerization. Impurities
such as oxygen, air, water, alcohols and the like must therefore be
excluded from the polymerizer since their presence serves to
terminate the growing polymer chains.
The polymerization will typically be conducted by charging the
initial monomer to the polymerizer which contains the initiator
system in a suitable solvent and conducting the polymerization for
a time necessary to insure substantially complete conversion of the
monomer. A second monomer will then be charged and polymerized. If
additional monomers are to be polymerized to form additional
blocks, the procedure will be repeated as required.
To recover the block polymers from the polymerization system
conventional techniques are employed. Typically, when the
polymerization of the final block segment is essentially complete,
a terminating (short-stopping) agent such as water, methanol,
ethanol or the like will be added in sufficient quantity to
terminate the reaction. If desired, larger quantities may be added
so that the polymer will be precipitated from the solution at the
same time. It is sometimes more convenient to add the short-stop in
quantities sufficient to terminate the polymerization but not
precipitate the polymer, then to add a stabilizing amount of a
material such as phenyl-.beta.-naphthylamine,
4-methyl-2,6-di-t-butylcresol or the like prior to the
precipitation of the polymer.
Employing the present initiator systems a wide variety of useful
block polymer compositions can be obtained by varying the monomers
employed, the number of block segments, the sequence of the block
segments and the molecular weight differences of the block
segments. The present invention is particularly useful for the
preparation of two- and three-block polymers. Heretofore there has
been no convenient means for obtaining such block polymers when the
block segments were derived from polar monomers.
Polar monomers which may be polymerized to obtain block polymers in
accordance with the present invention include acrylonitrile,
methacrylonitrile, alkyl acrylates and alkyl methacrylates wherein
the alkyl substituent contains from one to eight carbon atoms. Such
alkyl acrylates and methacrylates include ethyl acrylate, butyl
acrylate, 2-ethyl-hexyl acrylate, methyl methacrylate, ethyl
methacrylate, isopropyl methacrylate, 2-ethylhexyl methacrylate and
the like. The present process is particularly advantageous for the
formation of two- and three- block copolymers derived from
methacrylonitrile and methyl methacrylate. Block copolymers
containing more than three polymer block segments may also be
prepared in accordance with the present invention.
Any combination of the polar monomers may be block polymerized, in
any order, employing the present process. This is contrary to
previously known anionic processes where, if polar monomers could
be polymerized, they had to be either homopolymerized or
polymerized as the terminal block segment due to the tendency to
terminate the growing chains. The initiator systems of the present
invention permit the polymer anion obtained with polar monomers to
propagate freely with a minimum of termination.
The block copolymers obtained by the present invention are useful
in a wide variety of applications. They are typically thermoplastic
materials having excellent clarity, good low temperature properties
and solvent resistance, and are readily processable. The block
polymers may be molded or extruded into a variety of shaped
products. Shoe soles, weather seals and tubing constitute useful
applications for these block polymers. Solutions of these block
polymers can be used for impregnating fabrics to obtain useful
gasket compositions.
The following Examples serve to illustrate the invention more
fully. All parts and percentages are on a weight basis unless
otherwise indicated. Viscosities reported are intrinsic viscosities
measured at 30.degree. C. for a solution of the polymer prepared by
dissolving 0.1250 gram of the polymer in 25 ml
N,N-dimethylformamide.
In the Examples all solvents were distilled from calcium hydride
under a nitrogen atmosphere and passed through 4A molecular sieves
prior to use. The acrylonitrile, methacrylonitrile and alkyl
acrylate and methacrylate monomers were distilled from calcium
hydride and dried by passing through a 120 cm .times. 2 cm
molecular sieve column. All solvents and monomers were stored under
nitrogen.
The polymerization procedure, unless indicated to the contrary, was
to charge the polymerizer, which had been previously dried in an
oven at 120.degree. C. for a minimum of 18 hours and cooled and
sealed under a nitrogen atmosphere, first with the solvent, then
with the initiator and finally with the monomers. The organolithium
compound was mixed with the heterocyclic compound in the
polymerization solvent at room temperature. This solution was then
cooled to -50.degree. C. before the first monomer charge was made.
Other monomers were then sequentially added to the polymerizer. The
temperature of polymerization was -50.degree. C. and polymerization
times ranged between about 2 and 5 hours.
EXAMPLE I
Methyl methacrylate-methacrylonitrile block polymers were prepared
by the sequential polymerization of monomers employing an n-butyl
lithium/dibenzothiophene sulfone initiator system. The initiator
system was prepared by charging 0.5 mls (0.80 millimols) n-butyl
lithium to 40 mls toluene containing 0.10 gram dibenzothiophene.
Two polymerizations were conducted employing this initiator system.
In the first polymerization, 1 ml (9.0 millimol) methyl
methacrylate was initially charged to the polymerizer, allowed to
polymerize for approximately 2 hours, and 1 ml (12 millimol)
methacrylo-nitrile charged and the polymerization continued for an
additional 2 hours. In the second polymerization, 1 ml (12
millimol) methacrylonitrile was first charged, allowed to
polymerize, and 1 ml (9.0 millimol) methyl methacrylate added. Both
polymerizations were shortstopped after about four hours by the
addition of 1 ml of a 5 percent solution of HCl in methanol. The
polymers were precipitated with cold hexane and dried in a
50.degree. vacuum oven. Greater than 90 percent conversion of the
total monomers was achieved in both polymerizations and the
intrinsic viscosities of the polymers were 4.4 and 2.55,
respectively.
Block copolymerization was confirmed by gas chromatographic
analysis of the reaction mixture prior to the addition of the
second monomer and also prior to the addition of the short-stopping
agent. When the methacrylonitrile was employed as the first monomer
the conversion after 2 minutes time was nearly 60 percent and after
30 minutes polymerization about 95 percent or greater conversion
was obtained. The methacrylonitrile conversion was determined by
short-stopping at various reaction times and recovering the polymer
formed to that point and confirmed by vapor phase chromatographic
analysis of the polymerization mixture.
Employing similar polymerization techniques methyl
methacrylate-methacrylonitrile block copolymers were obtained with
this n-butyl lithium/dibenzothiophene sulfone initiator system
employing hexane as the polymerization solvent at -25.degree. C.
Also mixtures of hexane and toluene were found to be convenient and
useful polymerization media for conducting the present block
copolymerizations.
EXAMPLE II
Block polymerizations of methyl methacrylate and methacrylonitrile
were conducted using varying amounts of dibenzothiophene sulfone.
Three polymerizations were conducted. The recipes were as
follows:
A B C
__________________________________________________________________________
Toluene (mls) 40 40 40 n-Butyl lithium (mls) 0.5 0.5 0.5
Dibenzothiophene sulfone (grams) 0.03 0.05 0.07
__________________________________________________________________________
Each polymerizer was then charged with 1 ml (9.0 millimol) methyl
methacrylate and allowed to polymerize for one hour and followed by
1 ml (12 millimol) methacrylonitrile. The polymerizations were
continued for an additional 2 hours and short-stopped with 1 ml of
a 5% HCl/methanol solution. Near quantitative conversion of the
monomers was obtained with C. Block copolymers were also obtained
with A and B.
EXAMPLE III
Methacrylonitrile and methyl methacrylate were block polymerized as
follows: Three grams (14 millimol) dibenzothiophene sulfone and 12
mls (19 millimol) n-butyl lithium were charged at room temperature
to 1500 mls toluene charged in a liter polymerizer. The reactor and
its contents were cooled to about -50.degree. C. and 25 mls (225
millimol) methyl methacrylate added with stirring over about a 2
hour period. The polymerization was stirred for an additional 2
hours followed by the addition of 25 mls (300 millimol)
methacrylonitrile over 2 hours. After 16 hours the polymerization
was short-stopped with 5 mls of 5% HCl in methanol. The methyl
methacrylate-methacrylonitrile block copolymer was precipitated
with cold hexane, washed and dried at 50.degree. in a vacuum oven.
98 percent conversion of the monomers was obtained. The block
copolymer had a viscosity of 1.98 and glass transition temperatures
of 68.degree. C. and 98.degree. to 104.degree. C. Nitrogen analysis
showed 8.5 percent nitrogen present in the polymer which
corresponds to about 40 percent methacrylonitrile.
EXAMPLE IV
Employing the same procedure as described in Example III and the
same initiator system, methacrylonitrile (25 mls, 300 millimol) was
first polymerized for about 2 hours. Methyl methacrylate (25 mls,
225 millimol) was then added and the polymerization continued for
about 16 hours. The methacrylonitrilemethyl methacrylate block
copolymer obtained had an intrinsic viscosity of 1.11. The polymer
had glass transition temperatures of 62.degree. C. and 108.degree.
to 110.degree. C.
EXAMPLE V
Similarly, three-block copolymers were prepared by the sequential
polymerization of increments of methacrylonitrile, methyl
methacrylate and methacrylonitrile, in that order. 75 ml portions
of the monomers were employed for each charge. The polymerization
was conducted at -50.degree. C. and the polymerization times after
the addition of the first and second monomers was about one hour.
The total polymerization time was about 17 hours. The
methacrylonitrile-methyl methacrylate-methacrylonitrile three-block
copolymer was precipitated with acidified methanol and washed with
distilled water. The polymer was obtained as a colorless
powder.
EXAMPLE VI
A three-block copolymer methyl
methacrylate-methacrylonitrile-methyl methacrylate was prepared.
Seventy-five ml portions of the monomers were sequentially charged
to the 5 liter polymerizer containing 3400 ml toluene, 45 ml (72
millimol) n-butyl lithium and 12 grams (55.5 millimol)
di-benzothiophene sulfone. A 95.6 percent total conversion of the
monomers was obtained. The polymer contained 6.30 percent nitrogen
by analysis. Physical properties were obtained with an Instron
Tester on a sample of the polymer injection molded at 180.degree.
C. At a pull rate of 10 in/min. (room temperature) the polymer
elongated 3.5 percent, had a modulus of about 3.5 .times. 10.sup.5
and the tensile at break was about 11,400 psi.
EXAMPLE VII
Employing a similar procedure to that described in Example I,
acrylonitrile and ethyl acrylate were block copolymerized. Two
polymerizations were conducted. In the first, ethyl acrylate was
the initial monomer charge followed by acrylonitrile and, in the
second, acrylonitrile was the initial monomer charged followed by
ethyl acrylate. In both instances monomer conversions were high.
The resulting polymers were rubbery and could be elongated to
several times their original length.
EXAMPLE VIII
Methacrylonitrile and methyl methacrylate were block copolymerized.
The initiator system employed was prepared by charging 0.5 mls
(0.80 millimol) n-butyl lithium to 40 mls toluene containing 0.0650
gram (0.48 millimol) thianaphthene. Copolymerizations were
conducted both with methyl methacrylate as the initial monomer and
with methacrylonitrile as the initial monomer. High polymer yields
were obtained in both instances.
EXAMPLE IX
A dibenzothiophene/n-butyl lithium initiator system was prepared by
dissolving 0.4607 gram (2.5 millimol) dibenzothiophene in 200 mls
toluene. Forty mls (0.5 millimol dibenzothiophene) of this
solution, to which 0.5 ml (0.80 millimol) n-butyl lithium was
added, was used for the block copolymerization of methyl
methacrylate and methacrylonitrile. The block copolymer had a
slight yellowish coloration but was obtained in good yield with a
high intrinsic viscosity.
EXAMPLE X
Employing the same procedure as described in Example I,
methacrylonitrile and methyl methacrylate were block polymerized
with an n-butyl lithium/tetramethylene sulfone initiator system.
0.0603 gram (0.50 millimol) tetramethylene sulfone and 0.5 ml (0.80
millimol) n-butyl lithium was employed per 40 mls toluene. The
block copolymers obtained had intrinsic viscosities as high as
0.95.
EXAMPLE XI
Using the procedure of Example X except that 0.052 gram (0.50
millimol) tetramethylene sulfoxide was substituted for the
tetramethylene sulfone, methyl methacrylate and methacrylonitrile
were block copolymerized. Excellent monomer conversion was
obtained. The methyl methacrylate-methacrylo-nitrile block
copolymer had a viscosity of 1.81.
* * * * *